摘要
The catalytic partial oxidation of methane to syngas (CO+H2) has been simulated thermodynamically with the advanced process simulator PRO/Ⅱ. The influences of temperature,pressure,CH4/O2 ratio and steam addition in feed gas on the conversion of CH4 selectively to syngas and heat duty required were investigated, and their effects on carbon formation were also discussed. The simulation results were in good agreement with the literature data taken from a spouted bed reactor.
the catalytic partial oxidation of methane to syngas (CO + H_2)has been simulated thermodynamically with the advanced processsimulator PRO/II. The influences of temperature, pressure, CH_4/O_2ratio and steam addition in feed gas on the conversion of CH_4selectively to syngas and eat duty required were investigated, andtheir effects on carbon formation were also discussed. The simulationresults were in good agreement with the literature data taken from aspouted bed reactor.
基金
the China National Petroleum Co. (CNPC).
关键词
热力学
部分氧化催化
甲烷
合成气
methane
partial oxidation
syngas
thermodynamic simulation
